Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.
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METHOD OF TREATING SUBTERRANEAN FORMATIONS
TECHNICAL FIELD
The present disclosure relates to a method of treating a portion of a
subterranean
formation through the use of an aqueous fracturing fluid comprising dissolved
therein from 0.3 to 3.0 % by weight of a viscosifying agent, wherein said
viscosifying agent is a fast dissolving and easy dispersible unpurified
polygalactonnannan ether.
BACKGROUND OF THE ART
Hydraulic fracturing is widely used for stimulating petroleum and gas
production
and recovery from subterranean formations.
It involves the injection of a suitable fluid down a wellbore to reach a
formation;
the fluid shall be injected under sufficient pressure to extensively crack the
formation and to provide passageways for the oil and gas that are contained in
the pores spaces of the formation and help them flowing to the wellbore.
Suitable
particulate materials (proppants) are often injected into the formation to
prevent
the closure of the fractures.
Usually, fracturing fluids are gelled with water soluble polymers, especially
with
natural polymers or chemically modified natural polymers, such as etherified
natural polymers, to most effectively widen the fractures and inhibit fluid
loss,
Water soluble polymers are mainly available in powder form and must be
dissolved in the aqueous fluid to perform their viscosifying function.
Dissolution of natural polymer particles in aqueous fluids is typically
accompanied
by the formation of lumps; upon contact with water, a thin, sticky layer of
gel
forms on the surface of the particles preventing water from hydrating the
inner
part of the particles and favoring the formation of lumps.
As a consequence, the whole hydration step of the polymer is undesirably
prolonged, especially if the polymer shall be dissolved in large amounts of
saline
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aqueous fluids, which often happens in the preparation of aqueous fracturing
Among the natural polymers that are used to thicken fracturing fluids,
polygalactomannan gums and chemically modified polygalactomannan are widely
used, because they form strong gels in combination with crosslinkers that are
usually based on titanium, zirconium and boron salts.
Polygalactomannans (also called galactomannans) are polysaccharides obtained
from the endosperms of leguminosae seeds consisting of a mannose backbone
with galactose side groups (more specifically, a (1-4)-linked beta-D-
m nnannopyranose backbone with branchpoints from their 6-positions linked
to
alpha-D-galactose, i.e. 1-6-linked alpha-D-galactopyranose).
To provide a gelled fracturing fluid, polygalactomannan gums and chemically
modified polygalactomannans shall be previously dissolved in the aqueous
component of the fluid and then crosslinked with a crosslinking composition.
Unfortunately, also the dissolution of polygalactomannan gums and chemically
modified polygalactomannans, such as etherified polygalactomannans, suffer
from the disadvantages described above, i.e. the formation of lumps.
Many solutions have been put into practice to avoid lumping in the preparation
of
fracturing fluids, including apparatus that are specifically designed to
hydrate the
polymers and to continuously produce viscous treatment gel close to the oil
well
site, as it is known from US 2006/107998.
Another way to rapidly hydrate the viscosifying polymers is to prepare a
concentrated slurry of the polymer in a non-aqueous carrier fluid, usually a
hydrocarbon fluid, glycols or glycol derivatives, which facilitates the
polymer
dispersion and slurry mixing, but may represent a concern for the environment
and an additional cost.
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It is also well known in the art (by way of example from US 5,165,479) to
treat
natural gums with small amounts of crosslinking agents, such as glyoxal,
borates
and the like, to inhibit hydration and minimize the formation of lumps upon
contact with water.
US 3,808,195, by way of example, describes a process for rendering
polygalactonnannans and their water-soluble derivatives dispersible comprising
treating the gums and gum derivatives with boron salts.
US 3,297,583 describes a method for the rapid and lump-free dissolution of
many
macromolecular substances that involves the use of from 0.005% to 5% by
weight of aldehydes as crosslinking agents to improve dispersibility.
Although treatment with crosslinking agents is well known to improve
dispersibility of polygalactomannans, the net result of the treatment with
crosslinking agents disclosed by the prior art are polymers that are
dispersible
but have a dissolution time which may still be unsuitable for fracturing
operations.
Therefore, it would be highly desirable to provide a polygalactomannan which
is
readily soluble and can be used as viscosifying agent for aqueous based
fracturing fluids because of its fast dissolving characteristics and
dispersibility.
The polygalactomannan ethers commonly used in the field are purified products,
i.e. the reaction by-products have been removed by washing the reaction mass,
so that they usually contain more than 95 % by weight of active matter.
It has now been found that unpurified polygalactomannan ethers are more easily
dispersible and fast dissolving in fracturing fluid when compared to the
corresponding purified products. Unexpectedly, their impurities beneficially
affect
their dissolution rate and their dispersibility without impairing the
characteristics
required as viscosifying agent.
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With the expression "unpurified polygalactomannan ethers" we mean
polygalactomannan ethers which have not been washed after the etherification
and contain from 4 to 25 % by dry weight of the etherification reaction by-
products. The amount of the etherification reaction by-product (impurities) is
measured as the ash content, for carboxyalkyl or cationic ethers of
polygalactomannans, and as the sum of the ash content and the glycol and
polyglycol content for hydroxyalkyl or mixed ethers of polygalactomannans. In
the present text, with the expression "molar substitution" (MS), we mean the
average number of hydroxyalkyl substituents on each anhyclroglycosidic unit of
the polygalactomannan, which can be measured, for example, by 11-1-NMR.
With the expression "degree of substitution" (DS), we mean the average number
of substituted hydroxyl groups on each anhydroglycosidic unit of the
polygalactomannan, which can be measured, for example, by 1H-NMR.
DESCRIPTION OF THE INVENTION
In one aspect, the disclosure relates to a method of treating a portion of a
subterranean formation comprising:
a) providing an aqueous fracturing fluid comprising dissolved therein from 0.3
to
3.0 % by weight of a viscosifying agent, wherein said viscosifying agent is an
unpurified polygalactomannan ether containing from 4 to 25 % by dry weight
of impurities prepared according to the following process of etherification:
I) reacting a polygalactomannan with an etherifying agent in the presence of
an alkaline catalyst;
II) drying and recovering the unpurified polygalactomannan ether;
with the proviso that the process of etherification of the polygalactomannan
does not comprise any purification or washing step;
b) optionally adding a crosslinking composition;
c) placing the fracturing fluid into a portion of a subterranean formation.
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DETAILED DESCRIPTION OF THE INVENTION
The amount of impurities in the unpurified polygalactomannan ether is
calculated
as the sum of the ash content and the glycols and polyglycols content.
The ash content is determined at 900 C according to the ASTM D586-97(r02)
standard method. The glycol and polyglycol content, mainly consisting of di-
and
5 tri-
glycol, is determined by gas-chromatography with internal standardization
after extraction for 40 min at 40 C with acetone.
For the realization of the method of the present invention the unpurified
polygalactomannan ether preferably contains from 5 to 20 % by dry weight of
impurities.
Polygalactornannan ethers that can be used in the method of the invention are
hydroxyalkyl ethers of polygalactomannans, e.g. hydroxypropyl ethers and
hydroxyethyl ethers, ca rboxya I kyl ethers of polygalactomannans, e.g.
carboxymethyl ethers and carboxyethyl ethers, mixed carboxyalkyl and
hydroxyalkyl ethers of polygalactomannans, and cationic ethers of
polygalactomannans.
The etherification step I) of the invention is well known in the art.
Polygalactomannans suitable for the process of the invention may be extracted,
for example, from Trigonella foenum-graecum (fenugreek gum), Cyamopsis
tetragonoloba (guar gum), Cesalpinia spinosa (tara gum), Ceratonia siliqua
(locust bean gum or carob gum), Cassia tora and Cassia obtusifolia (cassia
gum).
These polygalactomannans differ from one another in the mannose-to-galactose
ratio. In order of increasing ratio, fenugreek gum has a mannose:galactose
ratio
about 1:1, guar gum about 2:1, tara gum about 3:1, locust bean gum or carob
gum about 4:1 and cassia gum about 5:1.
Step I) of the process of the present invention is applicable to
polygalactomannan
in the form of flour or in the form of "splits". The term "split" indicates
the
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endosperm which is obtained by removal of the hull and the germ from the
leguminosae seed.
Before the etherification, the polygalactonnannan splits or flour are usually
swelled or suspended in water or in a water/water soluble solvent mixture.
Suitable solvents are methanol, ethanol and secondary lower alkanols, such as
isopropanol, sec-butanol, sec-amyl alcohol, or tertiary lower alkanols.
The alkaline catalysts of step I) are in general alkali metal or alkaline
earth metal
hydroxides, such as sodium, potassium or calcium hydroxide.
Suitable etherifying agents for the preparation of hydroxyalkyl ethers of
polygalactomannans are alkylene oxides, e.g., ethylene oxide, propylene oxide,
butylene oxide to obtain hydroxyethyl polygalactomannans, hydroxypropyl
polygalactomannans or hydroxybutyl polygalactomannans.
Halo-carboxylic acids such as monochloroacetic acid or its salts can be used
for
the preparation of carboxyalkyl ethers.
Cationic ethers can be prepared using tertiary amino or quaternary ammonium
alkylating reagents such as 2-dialkylaminoethyl chloride, 3-chloro-2-
hydroxypropyltrimethyl ammonium chloride and 2,3-epoxy- propyltrimethyl
ammonium chloride.
Mixed ethers can be prepared adding mixture of the mentioned etherifying
agents.
The reaction can be conducted at room temperature or at elevated temperatures
for a time sufficient to complete the reaction, usually in from about 0.5 to
about
24 hours.
Thereafter, the pH of the resulting alkaline material can be reduced to a
neutral
or slightly acid value. Any acid may be selected to neutralize the reaction
mixture; examples of suitable acids are carbon dioxide, phosphoric acid,
sulfuric
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acid and acetic acid. The amount of acid used is the amount which is necessary
to reach the desired pH range.
The commercially available polygalactomannan ethers commonly used in the field
are purified after these steps by washing with water, an organic solvent, such
as
isopropanol or acetone, or a mixture of water and organic solvents.
On the contrary, the polygalactomannan ethers of the present invention are not
washed/purified and still contain by-products generated during their chemical
preparation (that is during etherification).
At the end of the process, the unpurified polygalactomannan ethers are dried
and
w recovered using means known in the art. Optionally the polygalactomannan
ethers can be milled before being dried.
The unpurified galactomannan ethers obtained from this process still contain
from
4 to 25% by dry weight of impurities as defined above.
More specific details about the preparation of the polygalactomannan ethers
can
be found, for example, in "Industrial Gums: Polysaccharides and their
Derivatives", 3rd Ed., Whistler, Roy L., and BeMiller, James N., Academic
Press
(1993).
The hydroxyalkyl ethers of polygalactomannans may have molar substitution
comprised between 0.1 and 2, preferably between 0.2 and 0.9, more preferably
between 0.3 and 0.6.
The carboxyalkyl ethers may have degree of substitution from 0.1 to 0.5,
preferably from 0.1 to 0.3.
The mixed ethers may have a MS and DS comprised in the same range of the
mono-ethers.
The cationic polygalactomannans may have degree of substitution from 0.1 to
0.5.
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In a preferred embodiment, the unpurified polygalactomannan ether has been
treated during the preparation process with a small amount of crosslinking
agent
and thus contains from 0.01 to 0.05% by weight, preferably from 0.02 to 0.04%
by weight, of crosslinking agent. Preferred crosslinking agent are glyoxal and
boron containing compounds.
A 1% by weight aqueous solution of the unpurified polygalactomannan ether to
be used in the method preferably exhibits a RVT Brookfield viscosity not
lower
than 500 mPa.s at 20 C and 20 rpm.
The unpurified polygalactomannan ethers of the disclosure preferably passes
for
95% of their weight through a 200 mesh standard sieve.
For the realization of the present invention guar is the preferred
polygalactomannan and hydroxypropyl guar, carboxymethyl guar and
carboxymethyl hydroxypropyl guar are the preferred polygalactomannan ethers.
The unpurified polygalactomannan ethers of the invention are fast hydrating
and
easily dispersible and can be advantageously used as viscosifying agents in
aqueous based fracturing fluids.
Any type of aqueous hydraulic fracturing fluid can be used in the method of
the
invention. The fluid can be, for example, a gelled fluid, including linear or
crosslinked gels, or a foamed gel, wherein foam bubbles help to transport and
to
place proppants into fractures.
In the method for treating a subterranean formation according to the
disclosure,
it is possible to add a crosslinking agent during the preparation of the
fluid. This
allows to substantially increase the viscosity of the polymer solution by
forming a
crosslinked polymer network in the aqueous based fluid. The crosslinking
agents
utilizable in the optional step b) are those commonly used in the field.
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While a variety of crosslinking agents can be utilized to crosslink the
thickened
aqueous fluid, preferred crosslinking agents include, but are not limited to,
boron
containing compounds and transition metal ion crosslinking agents.
Examples of boron crosslinking agents include: borate ion releasing compounds,
such as boric acid, boric oxide, pyroboric acid, metaboric acid, borax, sodium
tetraborate, pentaborate; ulexite, colemanite, and other slow dissolving
crosslinking borate minerals.
Transition metal ion crosslinking agents are, for example, zirconium and
titanium
releasing compounds, such as titanium dioxide, zirconium oxychloride,
zirconium
lactate, zirconium glycolate, zirconium lactate triethanolamine, zirconium
acetylacetonate, titanium citrate, titanium maleate, titanium tartrate, and
other
titanium and zirconium chelates.
If desired, mixtures of the crosslinking agents may be used in the
crosslinking
composition.
The aqueous component of the fracturing fluid may be selected from fresh
water,
salt water, seawater, natural or synthetic brine, mixtures of water and water
soluble organic compounds, any other aqueous liquid that does not interact
with
the other components of the well treatment fluid to adversely affect its
performance, and mixtures thereof.
Preferably the crosslinking compositions also comprise a delaying agent. These
delaying agents delay the rate of crosslinking reaction for a sufficient time
to
allow the aqueous thickened fluid to be easily pumped into the subterranean
zone
The aqueous fracturing fluid, beside the viscosifying agent, the crosslinking
composition and the aqueous component, normally contains additives that are
well known by those skilled in the art, such as proppants, gel breakers,
buffers,
clay stabilizers, oxygen scavengers, etc.
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Useful gel breakers include, but are not limited to, ammonium persulfate,
sodium
persulfate, sodium bromate and sodium chlorite, enzymes. Preferably, the gel
breaker is a delayed gel breaker, such as encapsulated ammonium persulfate. A
delayed gel breaker slowly releases the oxidizer from the polymer coating to
5 enable a strong initial gel to carry and to deposit the proppants in the
formation.
The fluid also optionally includes one or more proppants suspended in the
fluid.
Useful proppants include, but are not limited to, gravel, sand, resin coated
sand,
ceramic beads, bauxite, glass, glass beads and mixtures thereof.
The aqueous fracturing fluid also optionally includes one or more buffers.
Useful
10 buffers include, but are not limited to, potassium carbonate, sodium
carbonate,
potassium bicarbonate, sodium bicarbonate, sodium sesquicarbonate, potassium
sesquicarbonate, potassium hydroxide, sodium hydroxide, and mixtures thereof.
The buffer may be added to the fluid prior to adding the crosslinking
composition.
The aqueous fracturing fluid of the disclosure may optionally include one or
more
conventional additives that do not adversely affect the performance of the
well
treatment fluid. Such additives include, but are not limited to, clay
stabilizers, gel
stabilizers, surfactants, bactericides and the like.
Generally the thickened aqueous fracturing fluids of the invention have a Fann
viscosity of above about 50 mPa*s at 100 sec, and, more preferably, above
about 100 mPa.s at 100 sec-1.
In the method of the disclosure, the aqueous fracturing fluid is finally
pumped or
injected into the subterranean formation (e.g., from the surface through the
vvellbore). Preferably, the fluid is pumped or injected at a pressure
sufficient to
fracture the formation (e.g., generate a plurality of fractures) and thus to
enable
the particulate solid (proppants) suspended in the well treatment fluid to be
carried into the fractures and to be there deposited.
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The following examples are included to demonstrate preferred embodiments of
the invention.
EXAMPLES
Examples 1-5.
Preparation of purified and unpurified hydroxypropyl guar
800 g of guar flour or guar splits (see Table 1) were loaded in a 5 litres
stirred
reactor at room temperature. The reaction atmosphere was made inert by means
of vacuum/nitrogen washings, and, under vigorous stirring, different amounts
of
NaOH (see Table 1) and, for Examples 1-4, 2.5 g of borax in 440 g of
water/isopropanol were added. The mixture was maintained under stirring for 15
minutes at 20 C. The reactor was evacuated and refilled three times with
nitrogen then different amounts of propylene oxide (PO, see Table 1) were
added. The reaction mixtures were maintained for 45 minutes at 70-75 C under
stirring. Afterwards the reaction mass was cooled down to 40 C, the solvent
was
distilled off and the pH of the mass was brought down to a value comprised
between 9.0 and 10.0 by addition of CO2.
The reaction mass of the comparative Example 1 was purified after distillation
by
washing with water.
The hydroxypropyl guar so obtained were dried on a fluid bed drier using hot
air,
and milled. At the end of the process all the hydroxypropyl guar had a
moisture
content of about 3% by weight.
The MS, impurities and boron content and Brookfield RVT viscosity (1 % by
weight in water, 20 rpm, 20 C) of the hydroxypropyl guar of Examples 1-5 are
reported in Table 1, Boron content was determined, after acid digestion of the
polygalactomannan ethers, by inductively coupled plasma atomic emission
spectrometry (ICP-AES).
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Table 1
Guar NaOH PO MS Impurities Viscosity Boron
Sample (g) (g) % by wt. mPa.s (ppm)
Example 1* flour 89 187 0.42 1.8 4300 310
Example 2 flour SO 187 0.40 6.9 2420 249
Example 3 flour 34 155 0.42 11.1 2060 220
Example 4 split 33 155 0.42 7.3 2560 242
Example 5 flour 30 438 1.5 15.9 1100
* Comparative
Examples 6-8
Preparation of purified and unpurified carboxymethyl hydroxypropyl guar
800 g of guar flour were loaded in a 5 litres stirred reactor at room
temperature.
The reaction atmosphere was made inert by means of vacuum/nitrogen
washings, and, under vigorous stirring, different amounts of Na01-1, as
reported in
Table 2, 68.0 g of sodium chloroacetate and 2.5 g of borax in 350 g of
water/isopropanol were added. The mixture was maintained under stirring for 15
minutes at 20 C. The reactor was evacuated and refilled three times with
nitrogen then 120 g of propylene oxide were added. The reaction mixture was
maintained for 45 min at 70-75 C under stirring.
Afterwards the reaction system was cooled down to 40 C, the solvent was
distilled off and the pH of the reaction mass was brought down to a value
comprised between 9.0 and 10.0 by addition of CO2.
The reaction mass of the comparative Example 6 was purified after distillation
by
washing with water. The carboxymethyl hydroxypropyl guar so obtained were
dried on a fluid bed drier using hot air and milled. At the end of the process
all
the carboxymethyl hydroxypropyl guar of Example 6-8 had a moisture content of
about 3% by weight.
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The MS, DS, impurities and boron content, and Brookfield RVT viscosity (1% by
weight in water, 20 rpm, 20 C) of the carboxymethyl hydroxypropyl guar of
Examples 6-8 are reported in Table 2.
Table 2
NaOH
Impurities Viscosity Boron
Sample Guar MS DS
(B) Wo by wt mPa*s (PPm)
Example
flour 83 0.3 0.16 2.9 3300 260
6*
Example
flour 83 0.3 0.16 14.2 1930 215
7
Example
flour 54 0.3 0.18 6.8 2100 240
8
* Comparative
Applicative tests
The methods used in the application test are the following:
DISPERSIBILITY TEST
396 g of tap water and 4 g of sample were added in a 600 ml beaker without any
mixing. After 1 minute the mixture were stirred with a magnetic bar (5 cm
length) at 1200 rpm. After 1 minute the stirring was stopped and the solution
was checked visually in order to verify the presence of lumps or fish eyes
(small
translucent lumps). The results of the Dispersibility Test, reported in Table
3 and
Table 4, was considered positive (OK) if the solutions did not show lumps or
fish
eyes.
FANN TEST
For each sample of Examples 1-8, 500 ml of deionized water and 10 g of KCI
were transferred in a Waring Blender cup. The solution temperature was brought
to 24 C. The amounts of polygalactomannan ethers as indicated in Table 2 were
added to the solutions in 5 seconds under stirring at 2000 rpm. The pH of the
samples containing boron was adjusted with acetic acid to a value around 6.50.
Fann viscosity at 300 rpm was determined after exactly 2 min (VA.
The solution temperature was maintained at 24 C for 60 min after the
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dissolution. After this period the Fann viscosity at 300 rpm (VF) was
determined
setting the viscosimeter at 600 rpm for 15 seconds before the viscosity
determination. The hydration rate at 2 minutes, calculated as (V2/VF).100, is
reported in Table 3 for hydroxypropyl guar of Examples 1-5 (HPG) and in Table
4
for carboxymethyl hydroxypropyl guar of Examples 6-8 (CMHPG) (Hydration at 2'
(%).
Table 3
HPG
Sample (g/5 ml) Dispersibility Test Hydration at T (%)
00
Example 1* 2.40 OK 74
Example 2 2.57 OK 92
Example 3 2.83 OK 88
Example 4 2.64 OK 87
_
Example 5 3.00 OK 96
* Comparative
Table 4
CMHPG Dispersibility Test Hydration at 2' (0/0)
Sample (9/500 ml)
Example 6* 2.40 OK 91
Example 7 2.71 OK 98
Example 8 2.88 OK 95
* Comparative
The results show that the unpurified polygalactomannan ethers according to the
disclosure have excellent hydratability and dispersibility that make them
perfectly
suitable as viscosifier for aqueous based fracturing fluids.
On the contrary, the polygalactomannans ethers of the prior art do not possess
the same characteristics.
While the methods of this invention have been described in the terms of the
preferred embodiments, it will be apparent to those of skill in the art that
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variations may be applied to the process described herein without departing
from
the concept and scope of the invention. All such similar substitutes and
modifications obvious to those skilled in the art are deemed to be within the
scope of the invention as it is set out in the following claims.
